Technology Zone
Fluid filtration systems remove particles, water and contaminants from liquids and gases. This zone covers strainers, cartridge and bag filters, membranes, separators and the housings and automation behind them.
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A North Yorkshire manufacturer of industrial filtration systems has dramatically improved production times after introducing automation to a key process, with support from Made Smarter.
What this zone covers
Three ways to hold something back. A surface filter, a screen or a pleated cartridge, catches particles on the face at a defined rating and blinds when the face is covered. A depth filter, a bag or a wound cartridge, traps particles through its thickness and holds far more dirt at the price of a less exact cut. A membrane separates by pore size at the micron and nanometre scale and works with a cross flow rather than dead end.
In dead end filtration everything goes through the medium and the retained solids build a cake, so the differential rises until the element is changed. In cross flow the feed sweeps along the membrane and only part of it passes through, which keeps the surface clear and lets the process run continuously. Dead end is simple and cheap for low solids; cross flow earns its cost when the solids would blind a filter in an hour.
A nominal rating is a manufacturer's opinion; an absolute rating is a tested cut-off. The beta ratio makes it measurable: the number of particles upstream of a size divided by the number downstream, so beta 1000 at 10 micron means 99.9 % removal at that size. Comparing a nominal filter with an absolute one on price per element is comparing two different products.
Most filtration failures are a missing step upstream. A basket strainer takes out the pieces that would destroy a cartridge; a hydrocyclone or a centrifugal separator removes dense solids with no consumable at all; a coalescer takes water out of fuel and oil out of water. Putting one of these ahead of the fine stage usually costs less than the elements it saves in a season.
An element is either changed or cleaned, and the choice shapes the whole installation. Automatic backwash and self-cleaning filters keep running with no operator and suit continuous duties with steady solids. Cartridges are cheaper to buy and become a waste stream with a disposal cost. Membranes are cleaned in place on a chemical cycle, and the cleaning regime rather than the membrane usually decides how many years it lasts.
| Parameter | Typical range | Rule of thumb |
|---|---|---|
| Change-out differential | 1 to 2.5 bar above the clean pressure drop | Change on differential, not on the calendar; a blinded element can collapse |
| Clean pressure drop | 0.1 to 0.3 bar for a correctly sized housing | Record it after every change; a rising clean value means the wrong element |
| Cartridge flow rate | 1 to 3 m3/h per 10 inch element for water | Halve it for viscous product; flux, not housing size, sets the number of elements |
| Beta ratio | Beta 1000 equals 99.9 % removal at the stated size | Compare absolute ratings against each other, never against nominal ones |
| Cross flow velocity | 2 to 5 m/s along the membrane | Too low and the surface fouls, too high and you pay in pumping energy |
| Transmembrane pressure | 0.5 to 3 bar for ultrafiltration | If flux stops rising with pressure, the cake is controlling, not the membrane |
| Bag filter efficiency | Nominal 1 to 200 micron | Use bags as a dirt holding stage ahead of an absolute one |
| Clean in place cycle | Caustic then acid, 40 to 60 degrees, 30 to 60 minutes | Judge the cycle by whether the clean water flux returns, not by appearance |
| Symptom | Likely causes | What to do |
|---|---|---|
| Elements blind within days | No pre-filtration, rating too fine for the load, or a process upset upstream | Fit a strainer or a coarser first stage, review the rating, and trend the differential to find the upset |
| Differential stays low but quality is poor | Bypass around the element, a damaged seal, or a nominal element where absolute was specified | Check the seals and the hold-down, confirm the element seats, and verify the rating actually supplied |
| Clean pressure drop rises after every change | Wrong element fitted, housing partly fouled, or a valve not fully open | Record the clean drop each time, compare the element part number, and inspect the housing internals |
| Membrane flux falls and does not recover after cleaning | Irreversible fouling, wrong cleaning chemistry, or a cleaning temperature that was too low | Match the chemistry to the foulant, raise the temperature within the membrane limit, and measure clean water flux before and after |
| Filter housing leaks at the lid | Damaged o-ring, over-tightened clamp, or thermal cycling on a housing that was never designed for it | Replace the seal with the specified compound, tighten to the figure, and check the temperature range of the housing |
| Backwash uses more water than expected | Backwash triggered on time instead of on differential, or a screen that is being cleaned too aggressively | Trigger on differential with a maximum interval as backup, and tune the backwash duration to what the differential needs |
| Coalescer passes water downstream | Surfactants in the product, flow above the design rate, or a saturated element | Check for surfactant contamination, bring the flow back within rating, and drain the sump on a routine |
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What this zone covers
Absolute, whenever the specification has a number in it. A nominal rating is a manufacturer's description of typical performance and is not comparable between suppliers; an absolute rating is tested, usually expressed as a beta ratio. Beta 1000 at 10 micron means 99.9 % of particles at that size are removed. Nominal elements still have a place as a cheap dirt-holding stage ahead of the absolute one.
When a dead end filter would blind quickly. If the solids load is high, or the particles are soft and compressible, a cake forms and the differential climbs within hours. Cross flow sweeps the surface and runs continuously, and it also lets you concentrate rather than simply separate. The price is pumping energy, a cleaning regime and a more complicated plant.
On differential pressure, not on a schedule. Record the clean pressure drop after each change and set the change-out at roughly 1 to 2.5 bar above it. Leaving an element past that point risks collapsing it, which pushes everything it was holding straight downstream. A calendar interval is a fallback for elements nobody instruments, not a good practice.
Usually because there is no coarse stage in front of them. A basket strainer, a bag stage or a hydrocyclone takes out the material that a fine cartridge should never have seen, and it costs almost nothing per year. The other common cause is an upset upstream, which a differential trend will show as a step change rather than a gradual climb.
Three to seven years is common, and the cleaning regime decides where in that range you land. Fouling that is cleaned promptly and with the right chemistry is reversible; fouling left to consolidate is not. Measure clean water flux before and after each cleaning cycle: when it stops returning to its previous value, the membrane is ageing rather than dirty.
Rarely worth it. Depth cartridges hold dirt through their thickness and cleaning drives it deeper; pleated cartridges can sometimes be backflushed but lose integrity in the process. Where cleaning is genuinely wanted, use a filter designed for it: a self-cleaning screen, a backwashable candle or a metal element. Cleaning a disposable one usually costs more in downstream quality than it saves.
Surfactants, mostly. Anything that lowers the interfacial tension stops the small droplets joining into large ones, and a coalescer that worked for years will pass water the week after a new additive is introduced upstream. Flow above rating and a sump that is not drained are the other two, and both look like a failed element from the control room.
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